ES2350431A1 - Vineyard osmotolerante cect 13015 year and its application in the production and improvement of sweet wines and the obtaining of bioethanol. (Machine-translation by Google Translate, not legally binding) - Google Patents

Vineyard osmotolerante cect 13015 year and its application in the production and improvement of sweet wines and the obtaining of bioethanol. (Machine-translation by Google Translate, not legally binding) Download PDF

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ES2350431A1
ES2350431A1 ES200930240A ES200930240A ES2350431A1 ES 2350431 A1 ES2350431 A1 ES 2350431A1 ES 200930240 A ES200930240 A ES 200930240A ES 200930240 A ES200930240 A ES 200930240A ES 2350431 A1 ES2350431 A1 ES 2350431A1
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Juan Jose Moreno Vigara
Maria Teresa Garcia Martinez
Juan Carlos Garcia Mauricio
Rafael Andres Peinado Amores
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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12GWINE; PREPARATION THEREOF; ALCOHOLIC BEVERAGES; PREPARATION OF ALCOHOLIC BEVERAGES NOT PROVIDED FOR IN SUBCLASSES C12C OR C12H
    • C12G1/00Preparation of wine or sparkling wine
    • C12G1/02Preparation of must from grapes; Must treatment and fermentation
    • C12G1/0203Preparation of must from grapes; Must treatment and fermentation by microbiological or enzymatic treatment
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    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/14Fungi; Culture media therefor
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    • C12N1/18Baker's yeast; Brewer's yeast
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    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/02Preparation of oxygen-containing organic compounds containing a hydroxy group
    • C12P7/04Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
    • C12P7/06Ethanol, i.e. non-beverage
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

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Abstract

Cement 13015 osmotolerant wine yeast and its application in the production and improvement of sweet wines and the production of bioethanol, where a strain of saccharomyces cerevisiae cect 13015 is applied for the production of wines, especially sweet wines, as well as for the production of bioethanol from sugary substrates. This strain has been isolated from a fermented grape must by pedro ximºnez from the d.o. Montilla-moriles, and has been selected for its rapid fermentation kinetics, for its excellent organoleptic qualities, as well as for its high ethanol production. (Machine-translation by Google Translate, not legally binding)

Description

Levadura vínica osmotolerante CECT 13015 y su aplicación en la producción y mejora de vinos dulces y la obtención de bioetanol.Osmotolerant wine yeast CECT 13015 and its application in the production and improvement of sweet wines and obtaining of bioethanol.

La presente invención tiene por objeto la aplicación de una cepa de Saccharomyces cerevisiae CECT 13015 para la producción de vinos, especialmente vinos dulces, así como para la producción de bioetanol a partir de sustratos azucarados. Esta cepa ha sido aislada de un mosto fermentado de uva pasa Pedro Ximénez de la D.O. Montilla-Moriles, y ha sido seleccionada por su rápida cinética de fermentación, por sus excelentes cualidades organolépticas, así como por su elevada producción de etanol.The present invention aims at the application of a strain of Saccharomyces cerevisiae CECT 13015 for the production of wines, especially sweet wines, as well as for the production of bioethanol from sugary substrates. This strain has been isolated from a Pedro Ximénez fermented grape must from the DO Montilla-Moriles, and has been selected for its rapid fermentation kinetics, for its excellent organoleptic qualities, as well as for its high ethanol production.

Estado de la técnica anteriorPrior art

En algunas regiones cálidas, con especiales características climáticas, se obtienen vinos dulces especiales mejorando la calidad de las uvas recolectadas en su madurez, mediante un proceso de secado natural por exposición directa de las uvas al sol durante unos días. Esto sucede en regiones vitivinícolas con un índice heliotérmico de 2597ºC o superior, situadas en varios países mediterráneos como España, Grecia, Chipre, Italia y Turquía, donde se producen vinos de postre especiales por este método a partir de distintas variedades de uva, aunque principalmente se usan las variedades Muscat. En Andalucía (España) y particularmente en las zonas de Montilla-Moriles, Jerez y Málaga, se usa además de la uva Muscat, la uva Pedro Ximénez.In some warm regions, with specials climatic characteristics, special sweet wines are obtained improving the quality of the grapes harvested at maturity, through a natural drying process by direct exposure of the Grapes in the sun for a few days. This happens in wine regions with a heliothermal index of 2597 ° C or higher, located in several Mediterranean countries such as Spain, Greece, Cyprus, Italy and Turkey, where special dessert wines are produced by this method to from different grape varieties, although they are mainly used Muscat varieties. In Andalusia (Spain) and particularly in the areas of Montilla-Moriles, Jerez and Málaga, are In addition to the Muscat grape, the Pedro Ximénez grape.

El mosto obtenido de las uvas Pedro Ximénez en su madurez media posee un contenido en azúcares en torno a 25ºBx y después del proceso de pasificación presenta un contenido que alcanza hasta 45ºBx, equivalente a 500 g/L, (Franco M, Peinado RA, Medina M, Moreno J. 2004. Off-vine grape drying effect on volatile compounds and aromatic series in must from Pedro Ximénez grape variety. J Agrie Food Chem 52: 3905-3910).The must obtained from the Pedro Ximénez grapes at medium maturity has a sugar content of around 25ºBx and after the process of passification it presents a content that reaches up to 45ºBx, equivalent to 500 g / L, (Franco M, Peinado RA, Medina M, Moreno J. 2004. Off-vine grape drying effect on volatile compounds and aromatic series in must from Pedro Ximénez grape variety. J Agrie Food Chem 52 : 3905-3910).

Saccharomyces cerevisiae es un hongo sacarofílico y en su hábitat se encuentra con elevadas concentraciones de azúcares. Sin embargo, cuando se usa para fermentar mostos con alta concentración en azúcares se presentan una serie de problemas como son paradas de fermentación y fermentaciones lentas, que puede favorecer el desarrollo de microorganismos indeseables, que aumentan la acidez volátil y originan vinos de baja calidad (Caridi A., Crucitti P., Ramondino D. 1999. Winemaking of must at high osmotic strength by thermotolerant yeast. Biotechnol Lett, 21: 617-620). En Salmón JM, Mauricio JC. 1994. Relationship between sugar uptake kinetics and total sugar consumption in different industrial Saccharomyces cerevisiae strains during alcoholic fermentation. Biotechnol Lett 16: 89-94 se describe una menor actividad en el transporte de glucosa en levaduras que fermentan medios con una elevada concentración de azúcares. Con objeto de evitar estos problemas, algunos vinos dulces especiales se han elaborado tradicionalmente en determinadas zonas mezclando los mostos de uva pasificada con alcohol vínico. Este hecho origina problemas en la catalogación del producto en el mercado y para el consumidor final, ya que no ha sido elaborado mediante un proceso de fermentación. Una posible solución podría ser la realización de fermentaciones parciales dirigidas con levaduras aisladas y seleccionadas a partir de mostos de uva pasa. Saccharomyces cerevisiae is a saccharophilic fungus and in its habitat is found with high concentrations of sugars. However, when used to ferment musts with a high concentration of sugars, a series of problems occur, such as slow fermentation stops and fermentation, which can favor the development of undesirable microorganisms, which increase volatile acidity and produce low quality wines ( Caridi A., Crucitti P., Ramondino D. 1999. Winemaking of must at high osmotic strength by thermotolerant yeast. Biotechnol Lett , 21 : 617-620). In Salmon JM, Mauricio JC. 1994. Relationship between sugar uptake kinetics and total sugar consumption in different industrial Saccharomyces cerevisiae strains during alcoholic fermentation. Biotechnol Lett 16 : 89-94 describes a lower activity in the transport of glucose in yeasts that ferment media with a high concentration of sugars. In order to avoid these problems, some special sweet wines have been traditionally made in certain areas by mixing the must of grape with wine alcohol. This fact causes problems in the cataloging of the product in the market and for the final consumer, since it has not been elaborated through a fermentation process. A possible solution could be the realization of partial fermentations directed with isolated yeasts and selected from raisins.

La crisis energética causada por la dependencia de los combustibles fósiles, así como el efecto contaminante que éstos tienen sobre el ambiente, unido a su contribución al efecto invernadero, hace necesaria la búsqueda de fuentes energéticas alternativas o complementarias renovables, cuyo balance neto en la emisión de CO_{2} sea inferior (Cot M, Loret M-O, François J, Benbadis L. 2007. Physiological behaviour of Saccharomyces cerevisiae in aerated fed-batch fermentation for high level production of bioethanol. FEMS Yeast Res 7: 22-32). Una de estas fuentes energéticas es el bioetanol obtenido a partir de carbohidratos de plantas (Liang L, Zhang Y, Zhang L, Zhu M. Liang S, Huang Y. 2008. Study of sugarcane pieces as yeast supports for ethanol production from sugarcane juice and molasses. J Ind Microbiol Biotechnol 35: 1605-1613), que es particularmente interesante como combustible para vehículos automóviles bien sólo o mezclado con otros combustibles. El etanol se obtiene mediante un proceso en tres fases:The energy crisis caused by the dependence on fossil fuels, as well as the contaminating effect they have on the environment, together with their contribution to the greenhouse effect, makes it necessary to search for alternative or complementary renewable energy sources, whose net balance in the emission of CO2 is lower (Cot M, Loret MO, François J, Benbadis L. 2007. Physiological behavior of Saccharomyces cerevisiae in aerated fed-batch fermentation for high level production of bioethanol. FEMS Yeast Res 7 : 22-32). One of these energy sources is bioethanol obtained from plant carbohydrates (Liang L, Zhang Y, Zhang L, Zhu M. Liang S, Huang Y. 2008. Study of sugarcane pieces as yeast supports for ethanol production from sugarcane juice and molasses J Ind Microbiol Biotechnol 35 : 1605-1613), which is particularly interesting as fuel for motor vehicles either alone or mixed with other fuels. Ethanol is obtained through a three-phase process:

i) i)
obtención de una solución de azúcares fermentables,obtaining a solution of sugars fermentable,

ii) ii)
fermentación alcohólica de dicha solución, yalcoholic fermentation of said solution, Y

iii) iii)
destilación y deshidratación del etanol. La eficiencia del proceso total está fuertemente relacionada con la energía invertida, particularmente en la fase de destilación.distillation and dehydration of ethanol. The total process efficiency is strongly related to the inverted energy, particularly in the phase of distillation.

Se han usado distintas fuentes de carbohidratos fermentables, en función de su abundancia o disponibilidad en el entorno próximo o en los subproductos o residuos de la agricultura e industria local. De una forma inconsciente, se han usado sustratos como el maíz y el trigo, sin evaluar el impacto negativo que sobre la alimentación humana ha tenido la desviación de estos granos hacia la producción de bioetanol. Estos sustratos, ricos en almidón o carbohidratos, no asimilables directamente por los microorganismos fermentativos, requieren costosos pre-tratamientos ácidos o enzimáticos o calentamientos para convertir los carbohidratos no asimilables en azúcares fermentables (Leipper KA, Schlee C, Tebble I, Stewart GG. 2006. The fermentation of beet sugar syrup to produce bioethanol. J Inst Brew 112: 122-133.) que aumentan los costes de producción y la energía necesaria para obtener el etanol. El uso de sustratos que presenten altos contenidos en azúcares fermentables (melazas o jugos procedentes del proceso de extracción del azúcar de caña o de la remolacha) no requiere tratamientos especiales, por lo que el coste (económico y energético) del proceso será menor.Different sources of fermentable carbohydrates have been used, depending on their abundance or availability in the immediate environment or by-products or residues of local agriculture and industry. In an unconscious way, substrates such as corn and wheat have been used, without assessing the negative impact that the deviation of these grains towards bioethanol production has had on human food. These substrates, rich in starch or carbohydrates, not directly assimilable by fermentative microorganisms, require expensive acid or enzymatic pre-treatments or heating to convert non-assimilable carbohydrates into fermentable sugars (Leipper KA, Schlee C, Tebble I, Stewart GG. 2006 The fermentation of beet sugar syrup to produces bioethanol. J Inst Brew 112 : 122-133.) Which increase the production costs and the energy required to obtain ethanol. The use of substrates that have high content in fermentable sugars (molasses or juices from the process of extracting cane sugar or beet) does not require special treatments, so the cost (economic and energy) of the process will be lower.

Por otro lado, se sabe que cuanto mayor es el contenido en etanol de una mezcla, menor es el consumo energético necesario para su separación (Bertolini MC, Ernandes JR, Laluce C. 1991. New yeast strains for alcoholic fermentation at higher sugar concentration. Biotechnol Lett 13: 197-202). De este modo, cuanto mayor sea la concentración en etanol obtenida en la fase de fermentación, menor será la energía invertida en la destilación. En consecuencia, la optimización de la fase fermentativa con respecto al uso de microorganismos osmotolerantes que producen elevadas concentraciones de etanol a partir de sustratos con elevado contenido en azúcares se revela como una interesante alternativa para incrementar la eficiencia del proceso de obtención de bioetanol.On the other hand, it is known that the higher the ethanol content of a mixture, the lower the energy consumption necessary for its separation (Bertolini MC, Ernandes JR, Laluce C. 1991. New yeast strains for alcoholic fermentation at higher sugar concentration. Biotechnol Lett 13 : 197-202). Thus, the higher the concentration in ethanol obtained in the fermentation phase, the lower the energy invested in distillation. Consequently, the optimization of the fermentation phase with respect to the use of osmotolerant microorganisms that produce high concentrations of ethanol from substrates with high sugar content is revealed as an interesting alternative to increase the efficiency of the process of obtaining bioethanol.

La levadura Saccharomyces cerevisiae es el microorganismo más usado en la fermentación alcohólica, aunque en la actualidad la bacteria Zymomonas mobilis se está también usando debido a que tiene una serie de ventajas con respecto a S. cerevisiae (Zaldivar J, Nielsen J, Olsson L. 2001. Fuel ethanol production from lignocellulose: a challenge for metabolic engineering and process integration. Appl Microbiol Biotechnol 56: 17-34). Saccharomyces cerevisiae yeast is the most commonly used microorganism in alcoholic fermentation, although currently the Zymomonas mobilis bacteria is also being used because it has a number of advantages over S. cerevisiae (Zaldivar J, Nielsen J, Olsson L. 2001. Fuel ethanol production from lignocellulose: a challenge for metabolic engineering and process integration. Appl Microbiol Biotechnol 56 : 17-34).

Como ha sido previamente comentado S. cerevisiae es un hongo sacarofílico y en su hábitat se encuentra con elevadas concentraciones de azúcares. Sin embargo, cuando se usa para fermentar mostos con alta concentración en azúcares se presentan una serie de problemas como son paradas de fermentación y fermentaciones lentas (Caridi et al., 1999). Salmón y Mauricio (1994) han descrito una menor actividad en el transporte de glucosa en levaduras que fermentan medios con una elevada concentración de azúcares.As previously mentioned S. cerevisiae is a saccharophilic fungus and in its habitat is found with high concentrations of sugars. However, when used to ferment musts with a high concentration in sugars, a number of problems occur, such as slow fermentation stops and fermentation (Caridi et al ., 1999). Salmon and Mauricio (1994) have described a lower activity in the transport of glucose in yeasts that ferment media with a high concentration of sugars.

Para evitar estos problemas, una posible solución podría ser la realización de fermentaciones dirigidas con levaduras aisladas y seleccionadas a partir de medios muy azucarados como son los mostos de uva pasa, que alcanzan más de 400 g/L de azúcares fermentables. Normalmente, las cepas de levaduras implicadas en los procesos industriales tienen una osmotolerancia limitada, por lo que las fermentaciones se realizan a partir de concentraciones de azúcares inferiores al 20% (p/v). Por tanto, el uso de levaduras osmotolerantes y superproductoras de etanol es muy deseable en la producción de etanol.To avoid these problems, one possible solution could be the realization of fermentations directed with isolated and selected yeasts from very sugary media such as raisins, which reach more than 400 g / L of fermentable sugars. Normally, yeast strains involved in industrial processes have an osmotolerance limited, so fermentations are made from sugar concentrations below 20% (w / v). Therefore the use of osmotolerant yeasts and ethanol superproducers is very desirable in the production of ethanol.

La fermentación del mosto es un proceso microbiológico complejo que implica interacciones entre levaduras, bacterias y hongos filamentosos (Aranda A, Matallana E, del Olmo M. 2005. Levaduras. Saccharomyces I. Levaduras de primera fermentación. En Microbiología del vino, Coordinadores A. V. Carrascosa, R. Muñoz y R. González, pp 19-56. AMV Ediciones, Madrid). Tradicionalmente, la fermentación del mosto ha sido un fenómeno espontáneo, realizado por la microbiota que se encuentra en la superficie del grano de uva y en la bodega. Sin embargo, esta microbiota puede afectarse por un gran número de factores, como condiciones sanitarias, condiciones climáticas, grado de madurez de la cosecha, variedad de uva, uso de productos fitosanitarios, etc. Por tanto, las levaduras presentes en los frutos no son constantes a través de los años, ni tampoco sus características metabólicas que son, en gran medida, responsables de las características organolépticas del vino obtenido. Esta circunstancia da lugar a una variación, no deseada, de la producción de año en año. Para resolver este problema y también en un intento de obtener un producto parecido al producido en regiones tradicionalmente productoras, los países de nueva tradición vitivinícola iniciaron la fermentación con inóculos de levaduras seleccionadas e importadas de países con tradición muy arraigada. Se ha comprobado que el uso de levaduras seleccionadas tiene importantes ventajas con respecto a la fermentación espontánea tradicional. Sin embargo, es imposible obtener una cepa buena para cualquier tipo de vinificación, así, se han obtenido levaduras de distintas regiones productoras con el fin de obtener levaduras seleccionadas mejor aclimatadas a cada zona en cuestión. Hoy día, cada vez más se está imponiendo el uso de levaduras secas activas (LSA) seleccionadas para resolver distintos problemas. En general, las levaduras vínicas seleccionadas deben ser capaces de producir vinos de calidad. Y esta calidad debe mantenerse para un mismo tipo de mosto y procedimiento de elaboración, evitando la variabilidad y los problemas que pueden ocasionar los microorganismos silvestres no deseados. La utilización de levaduras seleccionadas en procesos de vinificación presenta básicamente cinco ventajas frente a la fermentación espontánea tradicional (Melero R. 1992. Fermentación controlada y selección de levaduras vínicas. Rev. Esp. Cienc. Tecnol. Aliment. 32, 371-379), que son: mayor velocidad de fermentación, máximo consumo de los azúcares reductores, mayor reproducibilidad en la calidad de los vinos, reducción de los problemas causados por levaduras extrañas silvestres, mayor control de la calidad sensorial del vino.The fermentation of the must is a complex microbiological process that involves interactions between yeasts, bacteria and filamentous fungi (Aranda A, Matallana E, Olmo M. 2005. Yeasts. Saccharomyces I. First fermentation yeasts. In Wine Microbiology, Carrascosa AV Coordinators , R. Muñoz and R. González, pp 19-56. AMV Ediciones, Madrid). Traditionally, the fermentation of the must has been a spontaneous phenomenon, carried out by the microbiota that is found on the surface of the grape grain and in the cellar. However, this microbiota can be affected by a large number of factors, such as sanitary conditions, climatic conditions, degree of maturity of the crop, grape variety, use of phytosanitary products, etc. Therefore, the yeasts present in the fruits are not constant throughout the years, nor are their metabolic characteristics that are, to a large extent, responsible for the organoleptic characteristics of the wine obtained. This circumstance gives rise to an unwanted variation in production from year to year. To solve this problem and also in an attempt to obtain a product similar to that produced in traditionally producing regions, countries with a new wine tradition began fermentation with selected yeast inoculums and imported from countries with deep-rooted tradition. It has been proven that the use of selected yeasts has important advantages over traditional spontaneous fermentation. However, it is impossible to obtain a good strain for any type of winemaking, thus, yeasts from different producing regions have been obtained in order to obtain selected yeasts better acclimatized to each area in question. Today, the use of active dry yeast (LSA) selected to solve different problems is increasingly being imposed. In general, selected wine yeasts should be able to produce quality wines. And this quality must be maintained for the same type of must and preparation procedure, avoiding the variability and problems that unwanted wild microorganisms can cause. The use of selected yeasts in winemaking processes has basically five advantages over traditional spontaneous fermentation (Melero R. 1992. Controlled fermentation and selection of wine yeasts. Rev. Esp. Cienc. Tecnol. Aliment. 32, 371-379), which are: higher fermentation speed, maximum consumption of reducing sugars, greater reproducibility in the quality of the wines, reduction of the problems caused by wild wild yeasts, greater control of the sensory quality of the wine.

Los criterios de selección de levaduras para su uso en enología son: baja producción de acidez volátil, consumo total de azucares fermentables, alto vigor fermentativo y máxima reducción de fase de latencia, capacidad fermentativa a altas y bajas temperaturas, resistencia al anhídrido sulfuroso, baja producción de anhídrido sulfuroso, baja producción de sulfhídrico, alta velocidad de sedimentación y capacidad de flocular, baja producción de espuma, fenotipo killer, baja producción de acetaldehído, producción de glicerol adecuada, producción de acetato de etilo y alcoholes superiores, asimilación de sustancias nitrogenadas, síntesis y excreción de aminoácidos y derivados amínicos, producción de \beta-glucosidasa, baja producción de precursores de carbamato de etilo. En la actualidad, existen más de 200 cepas comerciales de levaduras bien caracterizadas disponibles en el mercado (Schuller D, Casal M. 2005. The use of genetically modified Saccharomyces cerevisiae strains in the wine industry, Applied Microbiology and Biotechnology 68(3), 292-304). Actualmente, las investigaciones se dirigen fundamentalmente en tres sentidos: a) aislamiento de nuevas cepas locales, mejor aclimatadas a cada región productora, que permitan satisfacer las necesidades de cada bodeguero, b) obtención de cepas con propiedades específicas interesantes como: cepas floculantes, que se separen mejor de los vinos facilitando la clarificación, cepas con actividad \beta-glucosidasa, capaces de liberar terpenos responsables de aromas primarios varietales que mejoran las características organolépticas de ciertos vinos y c) introducción de marcadores genéticos específicos en las cepas seleccionadas para determinar y controlar el crecimiento de las mismas en mostos no estériles (Degré R. 1993. Selection and comercial cultivation of wine yeast and bacteria, in Wine Microbiology and Biotechnology, edited by G.H. Fleet, pp. 421-447, Harwood Academia Publishers).The criteria for selecting yeasts for use in oenology are: low production of volatile acidity, total consumption of fermentable sugars, high fermentative vigor and maximum reduction of latency phase, fermentation capacity at high and low temperatures, resistance to sulfur dioxide, low sulfur dioxide production, low hydrogen sulfide production, high sedimentation rate and flocculation capacity, low foam production, killer phenotype, low acetaldehyde production, adequate glycerol production, ethyl acetate production and higher alcohols, assimilation of nitrogenous substances , synthesis and excretion of amino acids and amino derivatives, production of β-glucosidase, low production of ethyl carbamate precursors. Currently, there are more than 200 well-characterized commercial yeast strains available in the market (Schuller D, Casal M. 2005. The use of genetically modified Saccharomyces cerevisiae strains in the wine industry, Applied Microbiology and Biotechnology 68 (3), 292 -304). Currently, the research is mainly directed in three ways: a) isolation of new local strains, better acclimated to each producing region, which allow to meet the needs of each winemaker, b) obtaining strains with specific interesting properties such as: flocculant strains, which Separate better from wines by facilitating clarification, strains with β-glucosidase activity, capable of releasing terpenes responsible for varietal primary aromas that improve the organoleptic characteristics of certain wines and c) introduction of specific genetic markers in the selected strains to determine and control their growth in non-sterile musts (Degré R. 1993. Selection and commercial cultivation of wine yeast and bacteria, in Wine Microbiology and Biotechnology, edited by GH Fleet, pp. 421-447, Harwood Academy Publishers).

Así pues, aunque existen bastantes LSA comerciales, teóricamente apropiadas para realizar vinificaciones, resulta mucho más adecuado utilizar cepas autóctonas (locales) seleccionadas, ya que aseguran su implantación como agente biológico más importante responsable de la fermentación alcohólica, además de mantener las características propias típicas de los vinos de la zona (Suarez JA, Iñigo B. 2003. Microbiología Enológica. Fundamentos de Vinificación. Ediciones Mundi-Prensa, Madrid). Esto se acentúa en aquellas zonas de climas cálidos donde las levaduras están adaptadas a la elevada concentración de azúcares, etanol y a altas temperaturas.So, although there are quite a few LSAs commercial, theoretically appropriate for vinifications, it is much more appropriate to use native (local) strains selected, since they ensure its implantation as a biological agent most important responsible for alcoholic fermentation, in addition to maintain the typical characteristics of the local wines (Suarez JA, Iñigo B. 2003. Oenological Microbiology. Fundamentals of Winemaking Mundi-Prensa editions, Madrid). This It is accentuated in those areas of warm climates where yeasts they are adapted to the high concentration of sugars, ethanol and high temperatures.

En la patente "Procedimiento de fermentación dirigida secuencial, nueva cepa de levadura que interviene en el mismo, y su aplicación industrial" (ES 2 222 786 A1) se hace referencia a un procedimiento de fermentación dirigida secuencial, por el cual el mosto es sembrado en tiempos diferentes por la cepa CECT 11773 de Pichia fermentans y por otra del género Saccharomyces. La primera da lugar a la síntesis de una gran cantidad de sustancias aromáticas y saborizantes con baja producción de etanol, que determinarán el aroma del producto final; la segunda levadura se encarga de terminar la fermentación aumentando la cantidad de alcohol acumulado hasta un 12-13% v/v. La aplicación en Enología de levaduras vínicas seleccionadas simplifica, desde el punto de vista microbiológico, el proceso de fermentación vínica y mejora su control.In the patent "Process of sequential directed fermentation, new strain of yeast involved in it, and its industrial application" (ES 2 222 786 A1) refers to a process of sequential directed fermentation, by which the must is sown at different times for the CECT 11773 strain of Pichia fermentans and for another of the Saccharomyces genus. The first results in the synthesis of a large amount of aromatic and flavoring substances with low ethanol production, which will determine the aroma of the final product; The second yeast is responsible for finishing the fermentation by increasing the amount of alcohol accumulated up to 12-13% v / v. The Enology application of selected wine yeasts simplifies, from the microbiological point of view, the wine fermentation process and improves its control.

El bioetanol es el alcohol etílico producido a partir de la fermentación de los azúcares que se encuentran en los productos vegetales (cereales, caña de azúcar, remolacha, etc) combinados en forma de sacarosa, almidón, hemicelulosa y celulosa. Principalmente, el microorganismo usado para llevar a cabo dicho proceso es S. cerevisiae. Actualmente, son numerosos los estudios enfocados a la producción de etanol como combustible a partir de fuentes renovables como alternativa económicamente viable a la gasolina. La mayoría de los estudios se centran en buscar la mejora de la eficiencia del proceso incrementando la velocidad de la producción de etanol, esto último está limitado por el microorganismo productor de etanol, debido al efecto tóxico de éste (Allain EJ. 2007. Cell-free ethanol production: The future of fuel ethanol. J Chem Technol Biotechnol 82: 117-124). En este sentido, son numerosos los trabajos de investigación encaminados a aislar y seleccionar distintas cepas silvestres de levaduras obtenidas de diversos sustratos como suelo, frutas maduras, melazas, alimentos fermentados, etc. (Kiran Sree N, Sridhar M, Suresh K, Banat IM, Venkateswar Rao L. 2000. High alcohol production by repeated batch fermentation using an immobilized osmotolerant Saccharomyces cerevisiae. 2000. J Ind Microbiol Biotechnol 24: 222-226; Brooks AA. 2008. Ethanol production potential of local yeast strains isolated from ripe banana peels. Afr J Biotechnol 7: 3749-3752; Gomes FCO, Silva CLC, Marini MM, Oliveira ES, Rosa CA. 2007. Use of selected indigenous Saccharomyces cerevisiae strains for the production of the traditional cachaca in Brazil. J Appl Microbiol 103: 2438-2447), existiendo en los últimos años un gran número de patentes en aspectos relacionados con organismos productores de etanol. También se han obtenido nuevas cepas mejoradas genéticamente (Knauf M, Kraus K. 2006. Specific yeast developed for modern ethanol production. 2006. Sugar Industry 131: 753-758; Seki T, Myoga S, Limtong S, Uedono S, Kumnuanta J, Taguchi H. 1983. Genetic construction of yeast strains for high etanol production. Biotechnol Lett 5: 351-356). Un microorganismo ideal para producir etanol debe tener un buen y rápido potencial fermentativo, capacidad de flocular, osmotolerancia apreciable, elevada tolerancia al etanol y buena termotolerancia (Knauf and Kraus, 2006, Chandel AK, Narasu M.L., Chandrasekhar G, Manikyam A., Rao LV. 2009. Use of Saccharum spontaneum (wild sugarcane) as biomaterial for cell immobilization and modulated ethanol production by thermotolerant Saccharomyces cerevisiae VS_{3}. Biores Technol 100: 2404-2410).Bioethanol is the ethyl alcohol produced from the fermentation of sugars found in plant products (cereals, sugar cane, beets, etc.) combined in the form of sucrose, starch, hemicellulose and cellulose. Mainly, the microorganism used to carry out this process is S. cerevisiae . Currently, there are numerous studies focused on the production of ethanol as fuel from renewable sources as an economically viable alternative to gasoline. Most studies focus on improving the efficiency of the process by increasing the speed of ethanol production, the latter is limited by the ethanol producing microorganism, due to its toxic effect (Allain EJ. 2007. Cell- free ethanol production: The future of fuel ethanol. J Chem Technol Biotechnol 82 : 117-124). In this sense, there are numerous research projects aimed at isolating and selecting different wild strains of yeasts obtained from various substrates such as soil, ripe fruits, molasses, fermented foods, etc. (Kiran Sree N, Sridhar M, Suresh K, Banat IM, Venkateswar Rao L. 2000. High alcohol production by repeated batch fermentation using an immobilized osmotolerant Saccharomyces cerevisiae . 2000. J Ind Microbiol Biotechnol 24 : 222-226; Brooks AA. 2008 Ethanol production potential of local yeast strains isolated from ripe banana peels Afr J Biotechnol 7 : 3749-3752; Gomes FCO, Silva CLC, Marini MM, Oliveira ES, Rosa CA. 2007. Use of selected indigenous Saccharomyces cerevisiae strains for the production of the traditional cachaca in Brazil. J Appl Microbiol 103 : 2438-2447), there being in recent years a large number of patents in aspects related to ethanol producing organisms. New genetically improved strains have also been obtained (Knauf M, Kraus K. 2006. Specific yeast developed for modern ethanol production. 2006. Sugar Industry 131 : 753-758; Seki T, Myoga S, Limtong S, Uedono S, Kumnuanta J, Taguchi H. 1983. Genetic construction of yeast strains for high ethanol production, Biotechnol Lett 5 : 351-356). An ideal microorganism to produce ethanol must have a good and fast fermentative potential, flocculability, appreciable osmotolerance, high ethanol tolerance and good thermotolerance (Knauf and Kraus, 2006, Chandel AK, Narasu ML, Chandrasekhar G, Manikyam A., Rao LV. 2009. Use of Saccharum spontaneum (wild sugarcane) as biomaterial for cell immobilization and modulated ethanol production by thermotolerant Saccharomyces cerevisiae VS_ {3}. Biores Technol 100 : 2404-2410).

Explicación de la invenciónExplanation of the invention.

Como ha sido indicado anteriormente, la fermentación de mostos de uva con elevados contenidos en azúcares para la elaboración de vinos dulces presenta una serie de problemas técnicos. Una posible solución podría ser la realización de fermentaciones dirigidas con levaduras osmotolerantes aisladas y seleccionadas de esos tipos de mostos. En la presente invención, se ha aislado y seleccionado una levadura natural de un mosto de uva pasa Pedro Ximénez con una concentración inicial de azúcares reductores de 450 g/L. Es una cepa de Saccharomyces cerevisiae, CECT 13015, y se caracteriza porque es osmotolerante y buena productora de etanol. Experimentos de microvinificación dirigida con esta levadura demuestra una cinética de fermentación más rápida y una mejora de las características organolépticas de estos vinos, con respecto a los obtenidos mediante fermentación espontánea. El uso de esta levadura vínica en la industria enológica podría ser útil para mejorar el aroma de los vinos, especialmente de los vinos dulces.As indicated above, the fermentation of grape must with high sugar content for the production of sweet wines presents a series of technical problems. A possible solution could be the realization of fermentations directed with isolated osmotolerant yeasts and selected from these types of musts. In the present invention, a natural yeast from a Pedro Ximénez grape must has been isolated and selected with an initial concentration of reducing sugars of 450 g / L. It is a strain of Saccharomyces cerevisiae , CECT 13015, and is characterized in that it is osmotolerant and a good producer of ethanol. Experiments of microvinification directed with this yeast demonstrates a faster fermentation kinetics and an improvement of the organoleptic characteristics of these wines, with respect to those obtained by spontaneous fermentation. The use of this wine yeast in the wine industry could be useful to improve the aroma of wines, especially sweet wines.

Por otro lado, en un segundo aspecto de la presente invención y debido a la creciente demanda de etanol por la crisis energética de los combustibles fósiles, se hace necesaria la búsqueda de cepas de levadura osmotolerantes y de elevada producción de etanol. La cepa CECT 13015 presenta un mayor crecimiento y cinética de fermentación en todas las fermentaciones ensayadas. Experimentos de microfermentación indican que esta levadura es de útil uso en la producción de bioetanol a partir de distintos sustratos azucarados como melazas o jugos obtenidos a partir de remolacha u otros.On the other hand, in a second aspect of the present invention and due to the growing demand for ethanol by the energy crisis of fossil fuels, the search for osmotolerant and high production yeast strains of ethanol The strain CECT 13015 shows greater growth and Fermentation kinetics in all fermentations tested. Microfermentation experiments indicate that this yeast is of Useful use in the production of bioethanol from different sugary substrates such as molasses or juices obtained from beet or others.

A lo largo de la descripción y las reivindicaciones la palabra "comprende" y sus variantes no pretenden excluir otras características técnicas, aditivos, componentes o pasos. Para los expertos en la materia, otros objetos, ventajas y características de la invención se desprenderán en parte de la descripción y en parte de la práctica de la invención. Los siguientes ejemplos y dibujos se proporcionan a modo de ilustración, y no se pretende que sean limitativos de la presente invención. Además, la presente invención cubre todas las posibles combinaciones de realizaciones particulares y preferidas aquí indicadas.Throughout the description and the claims the word "comprises" and its variants not they intend to exclude other technical characteristics, additives, components or steps. For those skilled in the art, other objects, advantages and features of the invention will be partly detached of the description and in part of the practice of the invention. The following examples and drawings are provided by way of illustration, and are not intended to be limiting of the present invention. In addition, the present invention covers all possible combinations of particular and preferred embodiments indicated herein.

Breve descripción de los dibujosBrief description of the drawings

Fig. 1 muestra la evolución de la masa volúmica (g/L) durante la fermentación con levadura osmo-etanol tolerante.Fig. 1 shows the evolution of the volumetric mass (g / L) during yeast fermentation osmo-tolerant ethanol.

Fig. 2 muestra las características de los vinos de uvas pasas Pedro Ximénez en donde (A) muestra las variables enológicas comunes, (características de los vinos), siendo 1: Etanol (% v/v), 2: A. volátil (g/l), 3: A. total (g/l). 4: pH v 5: d (q/ml) (B) los alcoholes superiores mayoritarios, (C) los compuestos carbonílicos y (D) polialcoholes mayoritarios, donde 6: vino tradicional, 7: control y 8: levadura CECT 13015.Fig. 2 shows the characteristics of the wines of Pedro Ximénez raisins where (A) shows the variables common oenological, (characteristics of the wines), being 1: Ethanol (% v / v), 2: A. volatile (g / l), 3: A. total (g / l). 4: pH v 5: d (q / ml) (B) Major higher alcohols, (C) Compounds carbonyl and (D) major polyalcohols, where 6: wine traditional, 7: control and 8: yeast CECT 13015.

Exposición detallada de modos de realización y ejemplosDetailed presentation of embodiments and examples

La presente invención se refiere al aislamiento y selección de una cepa de Saccharomyces cerevisiae, CECT 13015, para su aplicación en fermentaciones dirigidas para la producción de vinos dulces así como para la obtención de bioetanol a partir de sustratos azucarados.The present invention relates to the isolation and selection of a strain of Saccharomyces cerevisiae , CECT 13015, for application in fermentations directed for the production of sweet wines as well as for obtaining bioethanol from sugary substrates.

Aislamiento y selección de cepas osmotolerantesIsolation and selection of osmotolerant strains

Distintas cepas osmotolerantes de Saccharomyces cerevisiae se aislaron a partir de un mosto fermentado de uva secada al sol (450 g/L de azúcares fermentables iniciales) mediante el procedimiento de siembra por agotamiento en cajas de Petri con agar YPD (1% de extracto de levadura, 2% de peptona y 5% de glucosa, pH 5.5). Las cajas se incubaron a 28ºC durante 48 h. Posteriormente, cada colonia se pasó a un tubo con agar YPD inclinado para obtener un cultivo puro. Los cultivos puros se guardaron en nevera a 4ºC ó a -80ºC hasta su uso. Se ha seleccionado una cepa por sus características de osmo-etanol-tolerancia, buenas características organolépticas en mostos con elevado contenido en azúcares así como por la producción de etanol. La identificación y depósito de la cepa de levadura se llevó a cabo por la Colección Española de Cultivos Tipo (CECT), identificándose con el número CECT 13015.Different osmotolerant strains of Saccharomyces cerevisiae were isolated from a fermented must of sun-dried grapes (450 g / L of initial fermentable sugars) by the seeding procedure by depletion in Petri dishes with YPD agar (1% yeast extract , 2% peptone and 5% glucose, pH 5.5). The boxes were incubated at 28 ° C for 48 h. Subsequently, each colony was passed to a tube with inclined YPD agar to obtain a pure culture. The pure cultures were stored in a refrigerator at 4 ° C or at -80 ° C until use. A strain has been selected for its osmo-ethanol-tolerance characteristics, good organoleptic characteristics in musts with high sugar content as well as for ethanol production. The identification and deposit of the yeast strain was carried out by the Spanish Type Culture Collection (CECT), identifying with the number CECT 13015.

Mosto, correcciones prefermentativas, condiciones de fermentación e inoculación para la obtención de vinos dulcesWort, preferential corrections, conditions of fermentation and inoculation to obtain sweet wines

El mosto inicial de uva Pedro Ximénez pasa presentaba un valor de masa volúmica de 1,1543\pm0,0015 g/mL, equivalente a un contenido en azúcares reductores de 373\pm4 g/L y aproximadamente a 22% (v/v) de etanol potencial. El contenido en acidez titulable fue de 3,31\pm0.07 g/L, la acidez volátil 0,07\pm0.02 y el pH presentaba un valor de 4,30\pm0.02.The initial grape must Pedro Ximénez passes had a volumetric mass value of 1.1543 ± 0.0015 g / mL, equivalent to a content in reducing sugars of 373 ± 4 g / L and approximately 22% (v / v) of potential ethanol. The content in Titratable acidity was 3.31 ± 0.07 g / L, volatile acidity 0.07 ± 0.02 and the pH had a value of 4.30 ± 0.02.

El mosto se corrigió hasta un valor de pH de 3,8 mediante la adición de ácido tartárico y se añadió 50 mg/L de S02 como metabisulfito potásico y se dividió en 6 fracciones de 750 mL que se colocaron en sendas probetas de 1 L. Tres probetas se destinaron a un control sin fermentar, y 3 para la cepa CECT 13015. Las probetas se taparon con algodón hidrófobo y se sumergieron en un baño termostatizado con agua a 24ºC.The must was corrected to a pH value of 3.8 by the addition of tartaric acid and 50 mg / L of S02 was added as potassium metabisulfite and was divided into 6 750 mL fractions which were placed in individual 1L specimens. Three specimens were they were destined for an unfermented control, and 3 for strain CECT 13015. The specimens were covered with hydrophobic cotton and immersed in a thermostated bath with water at 24ºC.

Previamente a la inoculación, la cepa de S. cerevisiae CECT 13015 se puso a crecer por separado en medio YPD durante 24 horas a 28ºC y posteriormente se recogió por centrifugación y se lavó con agua destilada estéril y fría. El inoculo de cada levadura para cada probeta con mosto fue de 6\pm1x10^{6} células/mL.Prior to inoculation, the S. cerevisiae strain CECT 13015 was grown separately in YPD medium for 24 hours at 28 ° C and subsequently collected by centrifugation and washed with sterile and cold distilled water. The inoculum of each yeast for each test tube with must was 6 ± 1x10 6 cells / mL.

Producción de etanolEthanol production

La célula de levadura se cultivó en medio YPD (1% extracto de levadura, 2% peptona y 5% glucosa, pH 5.5) esterilizado en autoclave. Las células se incubaron a 24ºC en agitación continua a 200 rpm en un incubador Shaker (New Brunswick Scientific, UK) durante 24 h y se recogieron por centrifugación a 3500 x g.The yeast cell was cultured in YPD medium (1% yeast extract, 2% peptone and 5% glucose, pH 5.5) autoclaved. The cells were incubated at 24 ° C under continuous agitation at 200 rpm in a Shaker incubator (New Brunswick Scientific, UK) for 24 h and collected by centrifugation at 3500 x g .

Las microfermentaciones se llevaron a cabo a 24ºC en tubos Falcon de 50 mL con 20 ml de la solución 1% extracto de levadura, 2% peptona y concentraciones crecientes de glucosa de 25 a 45% (p/v). Los medios de fermentación se esterilizaron a vapor fluente durante 30 minutos. Los medios de fermentación se inocularon con 4x10^{6} cells/ml. Los tapones de los tubos Falcon se atravesaron con una aguja hipodérmica y se agitaron a 150 rpm.The microfermentations were carried out at 24 ° C in 50 mL Falcon tubes with 20 ml of the 1% extract solution of yeast, 2% peptone and increasing glucose concentrations of 25 to 45% (w / v). The fermentation media were steam sterilized fluent for 30 minutes. The fermentation media were inoculated with 4x10 6 cells / ml. The plugs of the Falcon tubes are they pierced with a hypodermic needle and stirred at 150 rpm.

El número de células totales se determinó por recuento en un contador electrónico de partículas (Beckman Coulter Z2 Particle Count and Size Analyzer). El desarrollo del proceso de fermentación se monitorizó por la cantidad de CO_{2} liberada como medida de pérdida de peso (Sablayrolles et al., 1987; Bely et al., 1990).The total cell number was determined by counting in an electronic particle counter (Beckman Coulter Z2 Particle Count and Size Analyzer). The development of the fermentation process was monitored by the amount of CO2 released as a measure of weight loss (Sablayrolles et al ., 1987; Bely et al ., 1990).

El etanol se cuantificó por el Kit enzimático de Boehringer-Mannheim, Alemania.Ethanol was quantified by the Enzymatic Kit of Boehringer-Mannheim, Germany.

Ejemplo 1Example 1 Obtención de vino dulceObtaining sweet wine

La Fig. 1 muestra la cinética de fermentación. El mosto inoculado con la cepa CECT 13015 mostró un valor de la masa volúmica de 1078 g/L a las 140 horas.Fig. 1 shows the fermentation kinetics. The must inoculated with strain CECT 13015 showed a mass value 1078 g / L volume at 140 hours.

El contenido final en etanol fue de un 12% (v/v) de etanol. En este momento se detuvo la fermentación mediante la adición de alcohol vínico hasta un contenido en etanol del 15% (v/v) y una masa volúmica de 1062 g/L para CECT 13015. Por otro lado, el control corresponde a la adición de alcohol vínico al mosto inicial hasta un valor del 10% (v/v) y se obtuvo un valor de 1153 g/L, que no se alteró durante todo el ensayo.The final ethanol content was 12% (v / v) of ethanol At this time the fermentation was stopped by addition of wine alcohol to an ethanol content of 15% (v / v) and a volumetric mass of 1062 g / L for CECT 13015. On the other hand, the control corresponds to the addition of wine alcohol to the initial must up to a value of 10% (v / v) and a value of 1153 g / L was obtained, which It was not altered throughout the trial.

En la Fig. 2 se representan los valores medios de los compuestos y fracciones cuantificadas en cada uno de los experimentos realizados y en una muestra de vino PX elaborado de la forma tradicional. En la Fig. 2A se destaca que los mostos parcialmente fermentados con CECT 13015 presentaron valores de la acidez volátil superiores a los que poseen los dos restantes mostos no fermentados.The average values are shown in Fig. 2 of the compounds and fractions quantified in each of the experiments performed and in a sample of PX wine made from the traditional way. In Fig. 2A it is noted that musts partially fermented with CECT 13015 presented values of the volatile acidity superior to those of the two remaining musts unfermented

La Fig. 2B muestra la concentración de alcoholes superiores mayoritarios y metanol, destacó la mayor producción de los mismos en relación con los otros mostos. Entre los compuestos carbonílicos cuantificados (Fig. 2C), destacó el contenido en acetoína del mosto control (no fermentado) y el contenido en acetato de etilo del vino elaborado de la forma tradicional. En cuanto a la producción de 2,3-butanodiol y de glicerina (Fig. 2D) ambos compuestos presentaron un mayor contenido en los mostos fermentados con CECT 13015.Fig. 2B shows the concentration of alcohols Majority superiors and methanol, highlighted the increased production of the same in relation to the other musts. Among the compounds quantified carbonyls (Fig. 2C), highlighted the content in acetoin of control wort (unfermented) and acetate content of ethyl wine made in the traditional way. Refering to production of 2,3-butanediol and glycerin (Fig. 2D) both compounds had a higher content in musts fermented with CECT 13015.

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Ejemplo 2Example 2 Obtención de BioetanolObtaining Bioethanol

1one

El medio usado para estudiar la producción de etanol contenía de 25 a 45% (p/v) de glucosa. Los resultados expuestos en la tabla anterior ponen de manifiesto que la cepa CECT 13015 podría utilizarse para la obtención de etanol debido a su elevada eficiencia.The medium used to study the production of Ethanol contained 25 to 45% (w / v) glucose. The results exposed in the previous table show that the strain CECT 13015 could be used to obtain ethanol due to its high efficiency

Claims (6)

1. Levadura vínica perteneciente a la especie Saccharomyces cerevisiae depositada en la colección española de cultivos tipo, con número de identificación CECT 13015.1. Wine yeast belonging to the Saccharomyces cerevisiae species deposited in the Spanish type crop collection, with identification number CECT 13015. 2. Levadura vínica de acuerdo con la reivindicación 1 caracterizada porque presenta una tolerancia osmótica comprendida entre 25-45% (p/v) de glucosa y una tolerancia al etanol de entre 12-15% (v/v).2. Wine yeast according to claim 1 characterized in that it has an osmotic tolerance between 25-45% (w / v) glucose and an ethanol tolerance between 12-15% (v / v). 3. Levadura vínica de acuerdo a las reivindicaciones anteriores caracterizada porque produce un máximo de 20% (v/v) de etanol a 28ºC.3. Wine yeast according to the preceding claims characterized in that it produces a maximum of 20% (v / v) ethanol at 28 ° C. 4. Uso de la levadura vínica de las reivindicaciones 1 a 3 para la producción de bebidas alcohólicas.4. Use of wine yeast from claims 1 to 3 for the production of beverages alcoholic 5. Uso de la levadura vínica de las reivindicaciones 1 a 3 para la producción de vinos dulces naturales.5. Use of wine yeast from claims 1 to 3 for the production of sweet wines natural 6. Uso de la levadura vínica de las reivindicaciones 1 a 3 en la producción de etanol a partir de sustratos azucarados mediante la inoculación al medio de 4x10^{6} células/mL de dichas levaduras.6. Use of wine yeast from claims 1 to 3 in the production of ethanol from sugary substrates by inoculation to the medium of 4x10 6 cells / mL of said yeasts.
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Publication number Priority date Publication date Assignee Title
ES2704201A1 (en) * 2017-09-14 2019-03-14 Tomsa Destil S L Saccharomyces cerevisiae strain and its use for the production of alcoholic products (Machine-translation by Google Translate, not legally binding)
WO2019053316A1 (en) * 2017-09-14 2019-03-21 Tomsa Destil, S.L. Strain of saccharomyces cerevisiae and use thereof for making alcoholic products
IT201900001239A1 (en) * 2019-01-28 2020-07-28 Hts Enologia Di Luigi Scavone APPARATUS AND METHOD FOR AUTOMATED YEAST NUTRITION DURING THE ALCOHOLIC FERMENTATION OF GRAPE MUST

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